CN202185199U - Crystallization microfilter - Google Patents
Crystallization microfilter Download PDFInfo
- Publication number
- CN202185199U CN202185199U CN2011201479208U CN201120147920U CN202185199U CN 202185199 U CN202185199 U CN 202185199U CN 2011201479208 U CN2011201479208 U CN 2011201479208U CN 201120147920 U CN201120147920 U CN 201120147920U CN 202185199 U CN202185199 U CN 202185199U
- Authority
- CN
- China
- Prior art keywords
- crystallization
- filter
- microfilter
- filter core
- pressure gauge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000002425 crystallisation Methods 0.000 claims abstract description 24
- 230000008025 crystallization Effects 0.000 claims abstract description 23
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims description 11
- 239000011505 plaster Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 abstract description 7
- 239000013078 crystal Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 3
- 229940095054 ammoniac Drugs 0.000 abstract 2
- 235000009508 confectionery Nutrition 0.000 abstract 2
- 239000010419 fine particle Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 16
- 229910021529 ammonia Inorganic materials 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Filtering Materials (AREA)
Abstract
The utility model relates to a filter, in particular to a crystallization microfilter. The crystallization microfilter comprises a mesh filtering chamber (1), filter paper (2), a filter element (3), a sealing cover (4), a feeding pipe(5), a discharging pipe (6), a pressure gauge (7), a deflation valve (8), an electrical pump (9) and a crystallization kettle (10) (seeing attachment for the detailed analysis), wherein the mesh filtering chamber and the filter element are connected through a guide pipe, the crystallization kettle, the pressure gauge, the deflation valve and the electrical pump are arranged at a discharging port respectively, and a plastic rod filter element is arranged in the mesh filtering chamber and is connected with a discharging guide pipe. When being crystallized, ammoniac candy liquid generates black particles and has large volume, by virtue of the crystallization microfilter, the rate of filtration is improved, fine particles can be filtered, and white and pure crystal bodies can be released when the ammoniac candy is crystallized; moreover, the crystallization microfilter has the advantages of small volume, flexibility, simplicity, independence and convenience in operation.
Description
Technical field
The utility model equipment belongs to chemical industry equipment, particularly filters the filter of ammonia sugar liquors.
Background technology
Its efficient of existing filter is low, and does not possess the practicality of field machining.
The utility model content
It is filter that the purpose of the utility model is to use a kind of crystallization simple in structure, that be easy to control, is a kind of filter, particularly a kind of ammonia sugar crystallization microstrainer, and it comprises net filter chamber and filter core; The net filter chamber links to each other with feed conduit, and discharging opening is respectively equipped with crystallization kettle, Pressure gauge, vent valve and electrical pump, is provided with the sticking plaster filter core in the net filter chamber, and filter core links to each other with material outlet canal.Because black particle can appear in the ammonia sugar liquors when crystallization, and the volume of ammonia sugar liquors is very big, so this spline filter had both improved the rate of filtration, also can be filled into molecule, can separate out very white very pure crystal when making the crystallization of ammonia sugar; In addition, the utility model is small and exquisite flexibly, and is simple independent, operates also very convenient:
Description of drawings
Fig. 1 is the structural representation of the utility model.
Label among the figure: 1-net filter chamber, 2-filter paper, 3-filter core, 4-seal cover, 5-feed pipe, 6-discharge nozzle, 7-Pressure gauge, 8-vent valve, 9-electrical pump, 10-crystallization kettle, the design drawing of specifically seeing Appendix.
The excellence that the utility model compared with prior art embodies is:
1, a kind of crystallization microstrainer is characterized in that: comprise net filter chamber and filter core; The net filter chamber links to each other with feed conduit, and discharging opening is respectively equipped with crystallization kettle, Pressure gauge, vent valve and electrical pump, is provided with the sticking plaster filter core in the net filter chamber, and filter core links to each other with material outlet canal.
2, seal cover is a flange form.
3, only use one deck filter paper covering filter core and can reach the filtration requirement, the time is short, and efficient is high.
4, have only a filter chamber, simple in structure, be easy to control, technology is advanced.
5, Pressure gauge, vent valve and electrical equipment pump link to each other with crystallization kettle, have reduced the structure of microstrainer, compare the equipment plug and play with conventional microstrainer.
The specific embodiment
Embodiment 1:
It comprises net filter chamber and filter core; The net filter chamber links to each other with feed conduit, and discharging opening is respectively equipped with crystallization kettle, Pressure gauge, vent valve and electrical pump, is provided with the sticking plaster filter core in the net filter chamber, and filter core links to each other with material outlet canal.Because black particle can appear in the ammonia sugar liquors when crystallization, and the volume of ammonia sugar liquors is very big, so this spline filter had both improved the rate of filtration, also can be filled into molecule, can separate out very white very pure crystal when making the crystallization of ammonia sugar; In addition, the utility model is small and exquisite flexibly, and is simple independent, operates also very convenient.
The high 100cm of filter cylinder, the high 90cm of filter core.Flange PP material DN125, filter core PP material DN125, filter cylinder PP material DN200.
Charging aperture on the filter cylinder is connected with the material outlet that will filter, the charging aperture of the discharging opening on the filter core with the material receiving tank is connected, open the receiving tank vacuum system, material is sucked in the receiving tank with vacuum; Filter cloth on the filter core or filter paper require to select according to material.
Claims (4)
1. a crystallization microstrainer is characterized in that: comprise net filter chamber, filter core and seal cover; The net filter chamber links to each other with feed conduit, and discharging opening is respectively equipped with crystallization kettle, Pressure gauge, vent valve and electrical pump, is provided with the sticking plaster filter core in the net filter chamber, and filter core links to each other with material outlet canal.
2. crystallization microstrainer according to claim 1 is characterized in that: said seal cover is a flange form.
3. crystallization microstrainer according to claim 1 is characterized in that: filter core only covers one deck filter paper.
4. crystallization microstrainer according to claim 1 is characterized in that: have only a filter chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201479208U CN202185199U (en) | 2011-05-04 | 2011-05-04 | Crystallization microfilter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201479208U CN202185199U (en) | 2011-05-04 | 2011-05-04 | Crystallization microfilter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202185199U true CN202185199U (en) | 2012-04-11 |
Family
ID=45916678
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201479208U Expired - Fee Related CN202185199U (en) | 2011-05-04 | 2011-05-04 | Crystallization microfilter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202185199U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105753240A (en) * | 2016-04-29 | 2016-07-13 | 华电郑州机械设计研究院有限公司 | Novel zero discharge treatment technology for high salinity wastewater of thermal power plant |
| CN106145498A (en) * | 2016-08-23 | 2016-11-23 | 华电郑州机械设计研究院有限公司 | A kind of thermal power plant high slat-containing wastewater zero-emission recovery and treatment method |
-
2011
- 2011-05-04 CN CN2011201479208U patent/CN202185199U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105753240A (en) * | 2016-04-29 | 2016-07-13 | 华电郑州机械设计研究院有限公司 | Novel zero discharge treatment technology for high salinity wastewater of thermal power plant |
| CN106145498A (en) * | 2016-08-23 | 2016-11-23 | 华电郑州机械设计研究院有限公司 | A kind of thermal power plant high slat-containing wastewater zero-emission recovery and treatment method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120411 Termination date: 20160504 |